Valorization of a Pulp Industry By-Product through the Production of Short-Chain Organic Acids

Detalhes bibliográficos
Autor(a) principal: Queirós, Diogo
Data de Publicação: 2017
Outros Autores: Sousa, Rita, Pereira, Susana, Serafim, Luísa Seuanes
Tipo de documento: Artigo
Idioma: eng
Título da fonte: Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)
Texto Completo: http://hdl.handle.net/10773/22651
Resumo: In this work, hardwood sulfite spent liquor (HSSL)—a by-product from a pulp and paper industry—was used as substrate to produce short-chain organic acids (SCOAs) through acidogenic fermentation. SCOAs have a broad range of applications, including the production of biopolymers, bioenergy, and biological removal of nutrients from wastewaters. A continuous stirred tank reactor (CSTR) configuration was chosen to impose selective pressure conditions. The CSTR was operated for 88 days at 30 °C, without pH control, and 1.76 days of hydraulic and sludge retention times were imposed. The culture required 46 days to adapt to the conditions imposed, reaching a pseudo-steady state after this period. The maximum concentration of SCOAs produced occurred on day 71—7.0 g carbon oxygen demand (COD)/L that corresponded to a degree of acidification of 36%. Acetate, propionate, butyrate, valerate, and lactate were the SCOAs produced throughout the 88 days, with an average proportion of 59:17:19:1.0:4.0%, respectively.
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spelling Valorization of a Pulp Industry By-Product through the Production of Short-Chain Organic AcidsShort-chain organic acidsHardwood sulfite spent liquorActivated sludgeAcidogenic fermentationMixed microbial culturesIn this work, hardwood sulfite spent liquor (HSSL)—a by-product from a pulp and paper industry—was used as substrate to produce short-chain organic acids (SCOAs) through acidogenic fermentation. SCOAs have a broad range of applications, including the production of biopolymers, bioenergy, and biological removal of nutrients from wastewaters. A continuous stirred tank reactor (CSTR) configuration was chosen to impose selective pressure conditions. The CSTR was operated for 88 days at 30 °C, without pH control, and 1.76 days of hydraulic and sludge retention times were imposed. The culture required 46 days to adapt to the conditions imposed, reaching a pseudo-steady state after this period. The maximum concentration of SCOAs produced occurred on day 71—7.0 g carbon oxygen demand (COD)/L that corresponded to a degree of acidification of 36%. Acetate, propionate, butyrate, valerate, and lactate were the SCOAs produced throughout the 88 days, with an average proportion of 59:17:19:1.0:4.0%, respectively.MDPI2018-03-15T12:33:17Z2017-05-12T00:00:00Z2017-05-12info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/articleapplication/pdfhttp://hdl.handle.net/10773/22651eng2311-563710.3390/fermentation3020020Queirós, DiogoSousa, RitaPereira, SusanaSerafim, Luísa Seuanesinfo:eu-repo/semantics/openAccessreponame:Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)instname:Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informaçãoinstacron:RCAAP2024-02-22T11:44:18Zoai:ria.ua.pt:10773/22651Portal AgregadorONGhttps://www.rcaap.pt/oai/openaireopendoar:71602024-03-20T02:56:43.042486Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos) - Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informaçãofalse
dc.title.none.fl_str_mv Valorization of a Pulp Industry By-Product through the Production of Short-Chain Organic Acids
title Valorization of a Pulp Industry By-Product through the Production of Short-Chain Organic Acids
spellingShingle Valorization of a Pulp Industry By-Product through the Production of Short-Chain Organic Acids
Queirós, Diogo
Short-chain organic acids
Hardwood sulfite spent liquor
Activated sludge
Acidogenic fermentation
Mixed microbial cultures
title_short Valorization of a Pulp Industry By-Product through the Production of Short-Chain Organic Acids
title_full Valorization of a Pulp Industry By-Product through the Production of Short-Chain Organic Acids
title_fullStr Valorization of a Pulp Industry By-Product through the Production of Short-Chain Organic Acids
title_full_unstemmed Valorization of a Pulp Industry By-Product through the Production of Short-Chain Organic Acids
title_sort Valorization of a Pulp Industry By-Product through the Production of Short-Chain Organic Acids
author Queirós, Diogo
author_facet Queirós, Diogo
Sousa, Rita
Pereira, Susana
Serafim, Luísa Seuanes
author_role author
author2 Sousa, Rita
Pereira, Susana
Serafim, Luísa Seuanes
author2_role author
author
author
dc.contributor.author.fl_str_mv Queirós, Diogo
Sousa, Rita
Pereira, Susana
Serafim, Luísa Seuanes
dc.subject.por.fl_str_mv Short-chain organic acids
Hardwood sulfite spent liquor
Activated sludge
Acidogenic fermentation
Mixed microbial cultures
topic Short-chain organic acids
Hardwood sulfite spent liquor
Activated sludge
Acidogenic fermentation
Mixed microbial cultures
description In this work, hardwood sulfite spent liquor (HSSL)—a by-product from a pulp and paper industry—was used as substrate to produce short-chain organic acids (SCOAs) through acidogenic fermentation. SCOAs have a broad range of applications, including the production of biopolymers, bioenergy, and biological removal of nutrients from wastewaters. A continuous stirred tank reactor (CSTR) configuration was chosen to impose selective pressure conditions. The CSTR was operated for 88 days at 30 °C, without pH control, and 1.76 days of hydraulic and sludge retention times were imposed. The culture required 46 days to adapt to the conditions imposed, reaching a pseudo-steady state after this period. The maximum concentration of SCOAs produced occurred on day 71—7.0 g carbon oxygen demand (COD)/L that corresponded to a degree of acidification of 36%. Acetate, propionate, butyrate, valerate, and lactate were the SCOAs produced throughout the 88 days, with an average proportion of 59:17:19:1.0:4.0%, respectively.
publishDate 2017
dc.date.none.fl_str_mv 2017-05-12T00:00:00Z
2017-05-12
2018-03-15T12:33:17Z
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
dc.type.driver.fl_str_mv info:eu-repo/semantics/article
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status_str publishedVersion
dc.identifier.uri.fl_str_mv http://hdl.handle.net/10773/22651
url http://hdl.handle.net/10773/22651
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv 2311-5637
10.3390/fermentation3020020
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